CA2930985C - Fluid loss additive for water based drilling fluids with improved thermal stability - Google Patents

Fluid loss additive for water based drilling fluids with improved thermal stability Download PDF

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Publication number
CA2930985C
CA2930985C CA2930985A CA2930985A CA2930985C CA 2930985 C CA2930985 C CA 2930985C CA 2930985 A CA2930985 A CA 2930985A CA 2930985 A CA2930985 A CA 2930985A CA 2930985 C CA2930985 C CA 2930985C
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polymer microsphere
monomers
polymer
hydrophobic
self
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CA2930985A
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French (fr)
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CA2930985A1 (en
Inventor
Weibin ZHA
Hui Zhou
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Halliburton Energy Services Inc
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Halliburton Energy Services Inc
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/02Well-drilling compositions
    • C09K8/03Specific additives for general use in well-drilling compositions
    • C09K8/035Organic additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F291/00Macromolecular compounds obtained by polymerising monomers on to macromolecular compounds according to more than one of the groups C08F251/00 - C08F289/00
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/50Compositions for plastering borehole walls, i.e. compositions for temporary consolidation of borehole walls
    • C09K8/504Compositions based on water or polar solvents
    • C09K8/506Compositions based on water or polar solvents containing organic compounds
    • C09K8/508Compositions based on water or polar solvents containing organic compounds macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/50Compositions for plastering borehole walls, i.e. compositions for temporary consolidation of borehole walls
    • C09K8/516Compositions for plastering borehole walls, i.e. compositions for temporary consolidation of borehole walls characterised by their form or by the form of their components, e.g. encapsulated material

Abstract

A polymer microsphere for use as a fluid loss additive in drilling muds including a hydrophobic core of hydrophobic monomers and a hydrophilic shell of hydrophilic monomers wherein the hydrophilic shell surrounds the hydrophobic core. The polymer microsphere is capable of forming micelles or microgels in water without using surfactants and can be block, graft, and random copolymers. The hydrophilic shell is physically or chemically linked to the hydrophobic core. The polymer microsphere further includes crosslinkers, preferably where the crosslinkers are monomers containing at least two ethylenically unsaturated groups.

Description

FLUID LOSS ADDITIVE FOR WATER BASED DRILLING FLUIDS WITH
IMPROVED THERMAL STABILITY
Inventors: Weibin Zha and Hui Zhou FIELD OF INVENTION
[0001] The embodiments disclosed herein relate generally to methods and compositions for fluid loss additives for polar solvent drilling fluids with improved thermal stability for use as fluid loss additives in oilfield applications.
BACKGROUND OF INVENTION
[0002] Polar solvent-based drilling fluids include water, ethylene glycol, propylene glycol, glycerol, N-methylpyrrolidone, and other solvents that are water soluble or miscible. Drilling muds can contain an oil soluble polymer in the form of a gel as fluid loss reducer. A process for preparing an oil soluble polymer fluid loss control agent may include the steps of dissolving at least one polymer in a hydrocarbon oil to form a clear solution or a gel, adding an emulsifier to the solution or the gel, and keeping the mixture under conditions of agitation until a clear creamy mixture is obtained.
Because of high temperature stability of the polymer used, this fluid loss agent can be used at high temperature and high pressure in water-based muds.
[0003] The use of oil soluble polymers with surfactants is distinct from using polymers made with hydrophobic and hydrophilic monomers. Usually oil soluble polymers/hydrophobic polymers have higher temperature stability than water soluble polymers/hydrophilic polymers. However, the present invention offers thermal stability of hydrophobic polymers while using hydrophilic polymers to help disperse the hydrophobic polymer in water instead of using surfactant.
DETAILED DESCRIPTION OF DISCLOSED EMBODIMENTS
[0004] As an initial matter, it will be appreciated that the development of an actual, real commercial application incorporating aspects of the disclosed embodiments will require many implementation-specific decisions to achieve the developer's ultimate goal for the commercial embodiment. Such implementation-specific decisions may include, and likely are not limited to, compliance with system-related, business-related, government-related and other constraints, which may vary by specific implementation, location and from time to time.
[0005]
While a developer's efforts might be complex and time-consuming in an absolute sense, such efforts would nevertheless be a routine undertaking for those of skill in this art having the benefit of this disclosure.
[0006] It should also be understood that the embodiments disclosed and taught herein are susceptible to numerous and various modifications and alternative forms.
Thus, the use of a singular term, such as, but not limited to, "a" and the like, is not intended as limiting of the number of items. Similarly, any relational terms, such as, but not limited to, "top," "bottom," "left," "right," "upper," "lower," "down," "up," "side,"
and the like, used in the written description are for clarity in specific reference to the drawings and are not intended to limit the scope of the invention.
[0007] In a selection of preferred embodiments, this disclosure describes the composition and preparation of self-dispersible polymer microspheres for use as fluid loss additives in oilfield applications.

[0007a] In accordance with an embodiment, there is provided a polymer microsphere for use as a fluid loss additive comprising: a hydrophobic core of hydrophobic monomers;
and a hydrophilic shell of hydrophilic monomers; wherein the hydrophilic shell surrounds the hydrophobic core, wherein the polymer microsphere forms micelles or microgels in water without using surfactants.
2a
[0008] This invention discloses embodiments including using block copolymers (such as polystyrene-b-polyethylene oxide), grafted copolymers or randomly copolymerized polymers with one water soluble monomer (such as N-vinylpyrrolidone) and one hydrophobic monomer (such as vinyl acetate) as fluid loss control additives for water-based drilling fluid systems. With one block (polyethylene oxide) soluble in water, the block copolymer can form micelles or microgels in water without using surfactant.
[0009]
These soft microgels will lower the permeability of filter cake so as to control the fluid loss. By controlling synthesis method, the microgels can also be made by random copolymerization or graft polymerization with water soluble monomer rich on the surface so that the microgels can be stabilized in water.
[0010] For example, the block copolymer may be the hydrophobic monomer with low Tg (low transformation temperature) to maintain the flexibility of the microgels. The majority of hydrophobic monomers in random copolymers have very limited direct contact with water so they are hydrolytically stable.
[0011] One embodiment of the present invention includes using block, grafted copolymer or random copolymers of hydrophilic and hydrophobic monomers as fluid loss control agent. Because these polymers can form microgels in water without an emulsifier, the procedure to use these polymers will be much easier than current practices.
These polymers may have high temperature stability so that they can be expected to be useful for drilling wells where the downhole temperature is higher than about 350 F.
[0012] Self-dispersible polymer microspheres are polymeric particles with a hydrophobic core surrounded by a layer of hydrophilic polymers. When added into water, these polymer microspheres are readily dispersed in the aqueous phase without the addition of emulsifiers.
[0013] The particle size of the polymer microspheres preferably ranges from about 0.01 to about 1000 microns. In a preferred embodiment to be used as an effective fluid loss control additive, the particle size is preferably between about 0.1 and about 100 microns.
[0014] The polymer microspheres can be block, graft, and random copolymers of hydrophobic and hydrophilic monomers, or can be a core-shell structure in which the hydrophobic core is surrounded by a hydrophilic shell. In the case of core-shell structure, the core and shell can be physically or chemically linked. The hydrophobic monomers generally refer to those with water solubility of less than about 100 g/L, whereas the hydrophilic monomers have water solubility higher than about 100 g/L at room temperature.
[0015]
Examples of hydrophobic monomers include styrene, substituted styrene, alkyl acrylatc, alkyl methacrylate, acrylonitrile, methacrylonitrile, N-alkyl acrylamide, N-alkyl methacrylamide, vinyl acetate, vinyl esters, N-vinylamides, isoprene, butadiene, diesters of maleic, fumaric, or itaconic acid.
[0016]
Examples of hydrophilic monomers include anionic, cationic, nonionic, and amphotcric monomers.
[0017]
Suitable anionic monomers include acrylic acid, methacrylic acid, maleic acid, fumaric acid, itaconic acid, monoesters of maleic, fumaric, or itaconic acid, sodium vinylsulfonate, sodium allyl or methallyl sulfonate, sodium styrenesulfonate, acrylamido-2-methylpropanesulfonic acid (AMPS), sodium 3 -allyloxy-2-hydroxypropane-1 -sulfonate (AHPS), and vinylphosphonic acid. Although the acids can be polymerized directly, they are generally neutralized with base from alkali metal hydroxide, alkaline earth metal hydroxide, ammonia, and amines before polymerization.
[0018]
Suitable cationic monomers generally contain an amine or ammonium group.
Examples of cationic monomers include 2-, 3- or 4-vinylpyridine, N-vinylimidazolc, 2-methyl-l-vinylimidazole, N-(3 -(dimethylamino)propyl) methacrylamide, 2-(diethylamino)ethyl methacrylate, (3-acrylamidopropyl)trimethylammonium chloride, diallyldimethylammonium chloride. The amine groups in the cationic monomers can be converted into quaternary ammonium by alkylating agents such as alkyl or aryl halides.
[0019]
Examples of nonionic monomers include acrylamide, methacrylamide, N-alkyl acrylamides or methacrylamides in which the alkyl group contains 1-3 carbons, N-[tri s (hydrox ym ethyl)methyl acryl am i de, N-vi nylpyrrol i done, N-vinylcaprolactam, monovinyl or monoallyl ethers of polyols (such as ethylene glycol monovinyl ether, ethylene glycol monoallyl ether, and glycerol monoallyl ether), mono-acrylates or methacrylates of poyols (such as 2-hydroxyethyl acrylate and poly(ethylene glycol) monomethacrylate), and N-vinylamides (such as N-vinylformamide and N-vinylacetamide). Note that the acrylate- and acrylamide-based monomers can be converted to anionic monomers after hydrolysis in water.
[0020]
Amphoteric monomers are monomers that contain both anionic and cationic groups. Examples of amphotcric monomers include betaine, sulfobetainc (or sultaine), and phosphobetaine-type monomers.
[0021] The amount of hydrophobic units in the polymer microspheres can be about 5% to about 95 % by weight, preferably about 10% to about 90% by weight, and most preferably about 20% to about 80% by weight.
[0022] The polymer microspheres can be crosslinked by the addition of crosslinkers during polymerization. Crosslinkers are monomers containing at least two ethylenically unsaturated groups. Examples of crosslinkers include methylenebisacrylamide, divinyl benzene, vinyl or ally! ethers of polyglycols or polyols, acrylate or methacrylate esters of polyglycols or polyols, divinylbenzene, vinyl or ally! acrylates and methacrylates, divinylimidazolidone, and dienes.
[0023] The amount of crosslinker can be about 0.01% to about 10% by weight, preferably about 0.05% to about 8% by weight, and most preferably about 0.1%
to about 6% by weight.
[0024] The polymers can be prepared by solution, suspension, precipitation, dispersion, or emulsion polymerization. Emulsion polymerization is the most common way of preparing polymer microspheres. Surfactant free emulsion polymerization is preferred.
[0025] In surfactant-free polymerization, the monomers are polymerized in the presence of ionic or ionizable monomers. Some of the monomers stabilize the polymers, thus obviating the need to use emulsifiers and/or protective colloids in the course of the emulsion polymerization. Surface-active compounds can be added to the polymerization reaction.
[0026]
Conventional emulsion polymerization is also applicable. In the conventional emulsion polymerization, emulsifiers or surfactants are used to disperse hydrophobic monomers into aqueous phase.
[0027] In a preferred embodiment to make the core-shell structure, the hydrophobic core can be synthesized first by emulsion polymerization. The surface of the core then can be modified or activated by physical (gamma rays) or chemical reactions so that a hydrophilic monomer can be further grafted on the hydrophobic core. The shell should be thick enough that the microspheres can be dispersed in water without agglomerate. To ensure the hydrophilic shell is thick enough, the weight of hydrophilic shell can be about 5% to about 95% by weight, preferably about 10% to about 90% by weight and most preferably about 20% to about 80% by weight.
[0028] A
polymer microsphere for use as a fluid loss additive including a hydrophobic core of hydrophobic monomers and a hydrophilic shell of hydrophilic monomers wherein the hydrophilic shell surrounds the hydrophobic core. The polymer microsphere preferably has a particle size of between about 0.01 to about 1000 microns and more preferably between about 0.1 and about 100 microns. The polymer microsphere is capable of forming micelles or microgels in water without using surfactants and can be block, graft, and random copolymers. The hydrophilic shell is physically or chemically linked to the hydrophobic core. The hydrophobic monomers are selected from a group consisting of styrene, substituted styrene, alkyl acrylate, alkyl methacrylate, acrylonitrile, methacrylonitrile, N-alkyl acrylamide, N-alkyl methacrylamide, vinyl acetate, vinyl esters, N-vinylamides, isoprene, butadiene, diesters of maleic, fumaric, and itaconic acid.
The hydrophilic monomers are selected from a group consisting of anionic, cationic, nonionic, and amphoteric monomers. The hydrophobic monomers in the polymer microsphere are about 5% to about 95 % by weight of the polymer microsphere.
The polymer microsphere further includes crosslinkers, preferably where the crosslinkers are monomers containing at least two ethylenically unsaturated groups, and wherein the amount of crosslinker is between about 0.01% to about 10% by weight of the polymer .. microsphere.
[0029] The preferred embodiment includes a method of preparing self-dispersible polymer microspheres for use as fluid loss additives, which includes the steps of forming a hydrophobic core of hydrophobic monomers and grafting hydrophilic monomers on the hydrophobic core to form a hydrophilic shell on the hydrophobic core. The method preferably uses emulsion polymerization free of surfactants. In a preferred embodiment, hydrophilic shell has a weight of between about 10% to about 70% by weight, of the polymer microsphere and/or each polymer microsphere has a particle size of between about 0.01 to about 1000 microns. In a most preferred embodiment, the polymer microsphere is capable of forming micelles or microgels in water without using surfactants.
[0030] The preferred method of use the invention is using a plurality of self-dispersible polymer microspheres as fluid loss additives, which include introducing the self-dispersible polymer microspheres into a drilling mud; where each self-dispersible polymer microsphere includes a hydrophobic core of hydrophobic monomers and a hydrophilic shell of hydrophilic monomers wherein the hydrophilic shell surrounds the hydrophobic core. The self-dispersible polymer microspheres are free of surfactants. The hydrophilic shell preferably has a weight of between about 10% to about 70% by weight of the self-dispersible polymer microspheres. Each self-dispersible polymer microsphere preferably has a particle size of between about 0.01 to about 1000 microns.
Each self-dispersible polymer microsphere preferably is selected from the group consisting of block, graft, and random copolymers. The hydrophilic shell is preferably physically or chemically linked to the hydrophobic core of each self-dispersible polymer microsphere.
[0031]
Therefore, the present embodiments are well adapted to attain the ends and advantages mentioned as well as those that are inherent therein. The particular embodiments disclosed above are illustrative only, as the present invention may be modified and practiced in different but equivalent manners apparent to those skilled in the art having the benefit of the teachings herein.
[0032] Furthermore, no limitations are intended to the details of construction or design herein shown, other than as described in the claims below. It is therefore evident that the particular illustrative embodiments disclosed above may be altered, combined, or modified and all such variations are considered within the scope and spirit of the present invention.
[0033] The invention illustratively disclosed herein suitably may be practiced in the absence of any element that is not specifically disclosed herein and/or any optional element disclosed herein. While compositions and methods are described in terms of "comprising," "containing," or "including" various components or steps, the compositions and methods can also "consist essentially of' or "consist of' the various components and steps.
[0034] All numbers and ranges disclosed above may vary by some amount.
Whenever a numerical range with a lower limit and an upper limit is disclosed, any number and any included range falling within the range is specifically disclosed. In particular, every range of values (of the form, "from about a to about b," or, equivalently, "from approximately a to b," or, equivalently, "from approximately a-b") disclosed herein is to be understood to set forth every number and range encompassed within the broader range of values.
[0035] Also, the terms in the claims have their plain, ordinary meaning unless otherwise explicitly and clearly defined by the patentee. Moreover, the indefinite articles "a" or "an," as used in the claims, are defined herein to mean one or more than one of the element that it introduces. If there is any conflict in the usages of a word or tenn in this specification and one or more patent or other documents, the definitions that arc consistent with this specification should be adopted.

100361 While the disclosed embodiments have been described with reference to one or more particular implementations, those skilled in the art will recognize that many changes may be made thereto without departing from the scope of the description.
Accordingly, each of these embodiments and obvious variations thereof is contemplated as falling within the scope described herein.

Claims (17)

1. A polymer microsphere for use as a fluid loss additive comprising:
a hydrophobic core of hydrophobic monomers; and a hydrophilic shell of hydrophilic monomers;
wherein the hydrophilic shell surrounds the hydrophobic core, wherein the polymer microsphere forms micelles or microgels in water without using surfactants.
2. The polymer microsphere of Claim 1 wherein each polymer microsphere has a particle size of between about 0.01 to about 1000 microns.
3. The polymer microsphere of Claim 1 or 2 wherein each polymer microsphere has a particle size of between about 0.1 and about 100 microns.
4. The polymer microsphere of any one of Claims 1 to 3 wherein each polymer microsphere is selected from the group consisting of block, graft, and random copolymers.
5. The polymer microsphere of any one of Claims 1 to 4 wherein the hydrophilic shell is physically or chemically linked to the hydrophobic core.
6. The polymer microsphere of any one of Claims 1 to 5 wherein the hydrophobic monomers are selected from a group consisting of styrene, substituted styrene, alkyl acrylate, alkyl methacrylate, acrylonitrile, methacrylonitrile, N-alkyl acrylamide, N-alkyl methacrylamide, vinyl acetate, vinyl esters, N-vinylamides, isoprene, butadiene, diesters of maleic, fumaric, and itaconic acid.
7. The polymer microsphere of any one of Claims 1 to 6 wherein the hydrophilic monomers are selected from a group consisting of anionic, cationic, nonionic, and amphoteric monomers.
8. The polymer microsphere of any one of Claims 1 to 7 wherein the hydrophobic monomers in the polymer microsphere are about 5% to about 95 % by weight of the polymer microsphere.
9. The polymer microsphere of any one of Claims 1 to 8 wherein the polymer microsphere further comprise a plurality of crosslinkers.
10. The polymer microsphere of Claim 9 wherein the crosslinkers are monomers containing at least two ethylenically unsaturated groups.
11. The polymer microsphere of Claim 10 wherein the amount of the crosslinkers is between about 0.01% to about 10% by weight of the polymer microsphere.
12. A method of using a plurality of self-dispersible polymer microspheres as fluid loss additives, which comprises the step of introducing the self-dispersible polymer microspheres into a drilling mud; where each self-dispersible polymer microsphere comprises:
a hydrophobic core of hydrophobic monomers; and a hydrophilic shell of hydrophilic monomers;
wherein the hydrophilic shell surrounds the hydrophobic core, wherein the polymer microsphere forms micelles or microgels in water without using surfactants.
13. The method of Claim 12 wherein the self-dispersible polymer microspheres are free of surfactants.
14. The method of Claim 12 or 13 wherein the hydrophilic shell has a weight of between about 10% to about 90% by weight of the self-dispersible polymer microspheres.
15. The method of any one of Claims 12 to 14 wherein each self-dispersible polymer microsphere microsphere has a particle size of between about 0.01 to about microns.
16. The method of any one of Claims 12 to 15 wherein each self-dispersible polymer microsphere is selected from the group consisting of block, graft, and random copolymers.
17. The method of any one of Claims 12 to 16 wherein the hydrophilic shell is physically or chemically linked to the hydrophobic core of each self-dispersible polymer microsphere.
CA2930985A 2013-12-26 2013-12-26 Fluid loss additive for water based drilling fluids with improved thermal stability Expired - Fee Related CA2930985C (en)

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Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10179872B2 (en) 2013-12-26 2019-01-15 Halliburton Energy Services, Inc. Fluid loss additive for water based drilling fluids with improved thermal stability
FR3037073B1 (en) * 2015-06-03 2017-07-14 Rhodia Operations AMPHIPHILIC POLYMERS FOR FILTRAT CONTROL
AU2015409182A1 (en) * 2015-09-15 2018-02-01 Halliburton Energy Services, Inc. Core-shell particles for treatment of subterranean formations
WO2018022554A1 (en) * 2016-07-26 2018-02-01 Board Of Regents, The University Of Texas System Microparticle carriers for aqueous compositions and methods of making
CN108929663B (en) * 2018-06-22 2020-11-27 陕西科技大学 Resin microsphere plugging agent and preparation method thereof
CN108997820B (en) * 2018-07-25 2022-01-07 华南师范大学 Dye microsphere, preparation method thereof, printing ink and electrowetting display device
CN111826141B (en) * 2019-04-23 2022-08-30 中国石油化工股份有限公司 Shell-and-film structure plugging material and preparation method thereof
CN110590985A (en) * 2019-07-30 2019-12-20 上海匡宇科技股份有限公司 Polymer microsphere and preparation method thereof
EP4031636A4 (en) * 2019-09-20 2022-10-26 Texas A&M University Degradable polymeric nanoparticles and uses thereof
CN110924894B (en) * 2019-11-20 2021-04-06 中国石油大学(北京) Exploitation method and profile control agent for heterogeneous low-permeability reservoir
CN111704697B (en) * 2020-05-29 2022-06-03 中国石油天然气股份有限公司 Core-shell type hyperbranched nano-polymer and preparation method thereof

Family Cites Families (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6107397A (en) 1997-03-24 2000-08-22 Basf Aktiengesellschaft Aqueous copolymer dispersions of water-soluble monomers with N-vinyl groups and hydrophobic monomers
US7677311B2 (en) * 2002-08-26 2010-03-16 Schlumberger Technology Corporation Internal breaker for oilfield treatments
EP1431368A1 (en) 2002-12-18 2004-06-23 Eliokem Fluid loss reducer for high temperature high pressure water-based mud application
US6858301B2 (en) * 2003-01-02 2005-02-22 Hewlett-Packard Development Company, L.P. Specific core-shell polymer additive for ink-jet inks to improve durability
DE10344975A1 (en) 2003-09-27 2005-04-21 Rhein Chemie Rheinau Gmbh Microgels in non-crosslinkable organic media
US7285582B2 (en) * 2004-12-30 2007-10-23 Conocophillips Company Modified latex drag reducer and processes therefor and therewith
US8012533B2 (en) * 2005-02-04 2011-09-06 Oxane Materials, Inc. Composition and method for making a proppant
AU2006294455B2 (en) * 2005-09-30 2013-06-20 Relypsa, Inc. Methods for preparing core-shell composites having cross-linked shells and core-shell composites resulting therefrom
US20080011476A1 (en) * 2006-07-11 2008-01-17 Halliburton Energy Services, Inc. Methods for coating particulates with tackifying compounds
US8822386B2 (en) 2010-06-28 2014-09-02 Baker Hughes Incorporated Nanofluids and methods of use for drilling and completion fluids
US20120270992A1 (en) * 2011-04-22 2012-10-25 Larock Richard C Surfactant-free core-shell hybrid latexes
US20140014348A1 (en) * 2011-08-31 2014-01-16 Self-Suspending Proppant Llc Self-suspending proppants for hydraulic fracturing
US9297244B2 (en) * 2011-08-31 2016-03-29 Self-Suspending Proppant Llc Self-suspending proppants for hydraulic fracturing comprising a coating of hydrogel-forming polymer
US20140000891A1 (en) * 2012-06-21 2014-01-02 Self-Suspending Proppant Llc Self-suspending proppants for hydraulic fracturing
US20130261032A1 (en) * 2012-03-29 2013-10-03 Schlumberger Technology Corporation Additive for subterranean treatment
US20140060831A1 (en) * 2012-09-05 2014-03-06 Schlumberger Technology Corporation Well treatment methods and systems
US20140151043A1 (en) * 2012-12-03 2014-06-05 Schlumberger Technology Corporation Stabilized fluids in well treatment
US10179872B2 (en) 2013-12-26 2019-01-15 Halliburton Energy Services, Inc. Fluid loss additive for water based drilling fluids with improved thermal stability

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GB201607657D0 (en) 2016-06-15
AU2013408844B2 (en) 2017-08-31
AR098910A1 (en) 2016-06-22
US10501675B2 (en) 2019-12-10
GB2534775A (en) 2016-08-03
GB2534775B (en) 2020-12-09
US10179872B2 (en) 2019-01-15
US20170022408A1 (en) 2017-01-26
US20190119547A1 (en) 2019-04-25
CA2930985A1 (en) 2015-07-02
AU2013408844A1 (en) 2016-05-26
WO2015099735A1 (en) 2015-07-02

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